Abstract
Pt/BEA–Al2O3 catalysts for the hydroisomerization of benzene-containing gasoline fractions are studied using a model feedstock (20% benzene and 80% n-heptane). The catalysts are prepared by varying the zeolite content from 5 to 70 wt % at a constant Pt loading of 0.3 wt % in all samples, with an aqueous H2PtCl6 solution being used as the Pt precursor. The acid properties of the samples are studied by means of temperature-programmed desorption (TPD). The effect of the support’s zeolite/binder ratio on the activity of the catalysts is determined: an increase in the zeolite content raises the system’s acidity and shifts the range of the reaction toward lower temperatures. The optimum zeolite/binder ratio is found to be 30% BEA/70% Al2O3. Changing the SiO2/Al2O3 ratio of the zeolite from 25 to 40 is shown to have no noticeable effect on catalyst activity. The use of the catalysts supported on 30% BEA/70% Al2O3 in the hydroisomerization of benzenecontaining gasoline fractions can be recommended for improving environmental performance.
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Original Russian Text © E.A. Belopukhov, I.M. Kalashnikov, M.D. Smolikov, D.I. Kir’yanov, T.I. Gulyaeva, A.S. Belyi, 2016, published in Kataliz v Promyshlennosti.
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Belopukhov, E.A., Kalashnikov, I.M., Smolikov, M.D. et al. Pt/BEA–Al2O3 catalysts for the isomerization of benzene/heptane mixtures. I: Optimizing the support’s composition. Catal. Ind. 9, 48–53 (2017). https://doi.org/10.1134/S2070050417010032
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DOI: https://doi.org/10.1134/S2070050417010032